EP0050505A2 - Dispositif pour mettre en contact un gaz et un liquide - Google Patents
Dispositif pour mettre en contact un gaz et un liquide Download PDFInfo
- Publication number
- EP0050505A2 EP0050505A2 EP81304870A EP81304870A EP0050505A2 EP 0050505 A2 EP0050505 A2 EP 0050505A2 EP 81304870 A EP81304870 A EP 81304870A EP 81304870 A EP81304870 A EP 81304870A EP 0050505 A2 EP0050505 A2 EP 0050505A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- liquid
- bed
- gas
- pressure drop
- auxiliary bed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/0278—Feeding reactive fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0492—Feeding reactive fluids
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/002—Apparatus for fixed bed hydrotreatment processes
Definitions
- the apparatus may comprise at least one gas by-pass conduit within the said vessel and extending through the auxiliary bed (e.g. from the bottom thereof) up to a level above the top of the liquid by-pass conduit and presenting a higher pressure drop for the passage of gas therethrough than the auxiliary bed when the latter is not fouled, whereby during operation, gas passes preferentially through the auxiliary bed when the pressure drop therethrough is less than the pressue drop through the gas by-pass conduit, and gas passes preferentially through the gas by-pass conduit when the pressure drop therethrough is exceeded by the pressure drop through the auxiliary bed.
- the pressure drop will be higher than 703.07 g/cm 2 (10 psi). In this illustration, the pressure drop will be, say 1.75768 kg/cm 2 (25 psi). Note that if all the tubes were of the same elevation above the bed and the gas and liquid flowed in the tubes as a two phase gas-liquid mixture, the bypassing pressure drop will be much higher than 1.75768 kg/cm 2 (25 psi).
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/198,793 US4313908A (en) | 1980-10-20 | 1980-10-20 | Catalytic reactor having bed bypass |
US198793 | 1980-10-20 | ||
US212755 | 1980-12-04 | ||
US06/212,755 US4330505A (en) | 1980-12-04 | 1980-12-04 | Hydroprocessing reactor with extended operating life |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0050505A2 true EP0050505A2 (fr) | 1982-04-28 |
EP0050505A3 EP0050505A3 (en) | 1982-08-18 |
EP0050505B1 EP0050505B1 (fr) | 1984-12-19 |
Family
ID=26894163
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19810304870 Expired EP0050505B1 (fr) | 1980-10-20 | 1981-10-19 | Dispositif pour mettre en contact un gaz et un liquide |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0050505B1 (fr) |
CA (1) | CA1160023A (fr) |
DE (1) | DE3167865D1 (fr) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0996499A1 (fr) * | 1997-06-30 | 2000-05-03 | Exxon Research And Engineering Company | Reacteur a contre courant |
EP1017488A1 (fr) * | 1997-06-30 | 2000-07-12 | Exxon Research And Engineering Company | Reacteur a contre courant |
FR2924950A1 (fr) * | 2007-12-17 | 2009-06-19 | Inst Francais Du Petrole | Plateau filtrant de predistribution avec tube deverseur pour reacteur a lit fixe a co-courant descendant de gaz et de liquide |
WO2019126420A1 (fr) | 2017-12-21 | 2019-06-27 | Uop Llc | Dispositif de collecte de dépôts pour réacteurs à courant descendant |
WO2019126432A1 (fr) | 2017-12-21 | 2019-06-27 | Uop Llc | Dispositif de collecte de tartre pour réacteurs à courant descendant |
EP3727632A4 (fr) * | 2017-12-21 | 2021-08-04 | Uop Llc | Dispositif de collecte de tartre pour réacteurs à courant descendant |
EP3727633A4 (fr) * | 2017-12-21 | 2021-09-01 | Uop Llc | Dispositif de collecte de dépôts pour réacteurs à courant descendant |
EP3727635A4 (fr) * | 2017-12-21 | 2021-09-08 | Uop Llc | Dispositif de collecte de tartre pour réacteurs à courant descendant |
WO2022187067A1 (fr) * | 2021-03-01 | 2022-09-09 | Chevron Phillips Chemical Company Lp | Dispositif de dérivation d'écoulement pour un récipient contenant des particules solides |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3425810A (en) * | 1965-05-03 | 1969-02-04 | Chevron Res | Hydrotreating apparatus |
US3524731A (en) * | 1968-09-30 | 1970-08-18 | Exxon Research Engineering Co | Mixed-phase flow distributor for packed beds |
US3607000A (en) * | 1969-04-17 | 1971-09-21 | Gulf Research Development Co | Internal bypass for a chemical reactor |
US3702238A (en) * | 1970-03-18 | 1972-11-07 | Gulf Oil Corp | Apparatus for by-passing reactants to the interior of a catalyst bed |
US3796655A (en) * | 1970-03-18 | 1974-03-12 | Gulf Oil Corp | Method for diminishing pressure drop within a catalyst bed |
US4126539A (en) * | 1977-12-05 | 1978-11-21 | Mobil Oil Corporation | Method and arrangement of apparatus for hydrogenating hydrocarbons |
-
1981
- 1981-10-19 EP EP19810304870 patent/EP0050505B1/fr not_active Expired
- 1981-10-19 DE DE8181304870T patent/DE3167865D1/de not_active Expired
- 1981-10-20 CA CA000388292A patent/CA1160023A/fr not_active Expired
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3425810A (en) * | 1965-05-03 | 1969-02-04 | Chevron Res | Hydrotreating apparatus |
US3524731A (en) * | 1968-09-30 | 1970-08-18 | Exxon Research Engineering Co | Mixed-phase flow distributor for packed beds |
US3607000A (en) * | 1969-04-17 | 1971-09-21 | Gulf Research Development Co | Internal bypass for a chemical reactor |
US3702238A (en) * | 1970-03-18 | 1972-11-07 | Gulf Oil Corp | Apparatus for by-passing reactants to the interior of a catalyst bed |
US3796655A (en) * | 1970-03-18 | 1974-03-12 | Gulf Oil Corp | Method for diminishing pressure drop within a catalyst bed |
US4126539A (en) * | 1977-12-05 | 1978-11-21 | Mobil Oil Corporation | Method and arrangement of apparatus for hydrogenating hydrocarbons |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0996499A1 (fr) * | 1997-06-30 | 2000-05-03 | Exxon Research And Engineering Company | Reacteur a contre courant |
EP1017488A1 (fr) * | 1997-06-30 | 2000-07-12 | Exxon Research And Engineering Company | Reacteur a contre courant |
EP0996499A4 (fr) * | 1997-06-30 | 2002-06-19 | Exxonmobil Res & Eng Co | Reacteur a contre courant |
EP1017488A4 (fr) * | 1997-06-30 | 2002-06-19 | Exxonmobil Res & Eng Co | Reacteur a contre courant |
FR2924950A1 (fr) * | 2007-12-17 | 2009-06-19 | Inst Francais Du Petrole | Plateau filtrant de predistribution avec tube deverseur pour reacteur a lit fixe a co-courant descendant de gaz et de liquide |
WO2009092875A2 (fr) * | 2007-12-17 | 2009-07-30 | Ifp | Plateau filtrant de predistribut1on avec tube deverseur pour reacteur a lit fixe a co-courant descendantde gaz et de liquide |
WO2009092875A3 (fr) * | 2007-12-17 | 2009-10-29 | Ifp | Plateau filtrant de predistribut1on avec tube deverseur pour reacteur a lit fixe a co-courant descendantde gaz et de liquide |
CN101918100A (zh) * | 2007-12-17 | 2010-12-15 | Ifp公司 | 用于以气液下降并流方式操作的固定床反应器的具有溢流管的预分布过滤板 |
RU2476255C2 (ru) * | 2007-12-17 | 2013-02-27 | Ифп | Фильтрующая тарелка предварительного распределения с переливной трубой для реактора с неподвижным слоем и параллельными нисходящими потоками газа и жидкости |
CN101918100B (zh) * | 2007-12-17 | 2013-03-20 | Ifp公司 | 用于以气液下降并流方式操作的固定床反应器的具有溢流管的预分布过滤板 |
US8487151B2 (en) | 2007-12-17 | 2013-07-16 | IFP Energies Nouvelles | Process and apparatus for filtration and pre-distribution of gas and liquid phases in a down-flow catalytic reactor |
WO2019126420A1 (fr) | 2017-12-21 | 2019-06-27 | Uop Llc | Dispositif de collecte de dépôts pour réacteurs à courant descendant |
WO2019126432A1 (fr) | 2017-12-21 | 2019-06-27 | Uop Llc | Dispositif de collecte de tartre pour réacteurs à courant descendant |
EP3727632A4 (fr) * | 2017-12-21 | 2021-08-04 | Uop Llc | Dispositif de collecte de tartre pour réacteurs à courant descendant |
EP3727675A4 (fr) * | 2017-12-21 | 2021-09-01 | Uop Llc | Dispositif de collecte de dépôts pour réacteurs à courant descendant |
EP3727633A4 (fr) * | 2017-12-21 | 2021-09-01 | Uop Llc | Dispositif de collecte de dépôts pour réacteurs à courant descendant |
EP3727635A4 (fr) * | 2017-12-21 | 2021-09-08 | Uop Llc | Dispositif de collecte de tartre pour réacteurs à courant descendant |
EP3727634A4 (fr) * | 2017-12-21 | 2021-09-08 | Uop Llc | Dispositif de collecte de tartre pour réacteurs à courant descendant |
US11224849B2 (en) | 2017-12-21 | 2022-01-18 | Uop Llc | Scale collection device for downflow reactors |
US11298669B2 (en) | 2017-12-21 | 2022-04-12 | Uop Llc | Scale collection device for downflow reactors |
WO2022187067A1 (fr) * | 2021-03-01 | 2022-09-09 | Chevron Phillips Chemical Company Lp | Dispositif de dérivation d'écoulement pour un récipient contenant des particules solides |
Also Published As
Publication number | Publication date |
---|---|
CA1160023A (fr) | 1984-01-10 |
DE3167865D1 (en) | 1985-01-31 |
EP0050505B1 (fr) | 1984-12-19 |
EP0050505A3 (en) | 1982-08-18 |
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Legal Events
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